EP1340536A2 - Utilisation de corps moulés - Google Patents

Utilisation de corps moulés Download PDF

Info

Publication number
EP1340536A2
EP1340536A2 EP03002949A EP03002949A EP1340536A2 EP 1340536 A2 EP1340536 A2 EP 1340536A2 EP 03002949 A EP03002949 A EP 03002949A EP 03002949 A EP03002949 A EP 03002949A EP 1340536 A2 EP1340536 A2 EP 1340536A2
Authority
EP
European Patent Office
Prior art keywords
particle size
particles
size range
range
moldings
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP03002949A
Other languages
German (de)
English (en)
Other versions
EP1340536A3 (fr
EP1340536B1 (fr
Inventor
Karlheinz Schaber
Arthur Heberle
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
RVT Process Equipment GmbH
Original Assignee
Rauschert Verfahrenstechnik GmbH
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Rauschert Verfahrenstechnik GmbH filed Critical Rauschert Verfahrenstechnik GmbH
Publication of EP1340536A2 publication Critical patent/EP1340536A2/fr
Publication of EP1340536A3 publication Critical patent/EP1340536A3/fr
Application granted granted Critical
Publication of EP1340536B1 publication Critical patent/EP1340536B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/32Packing elements in the form of grids or built-up elements for forming a unit or module inside the apparatus for mass or heat transfer
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/30Loose or shaped packing elements, e.g. Raschig rings or Berl saddles, for pouring into the apparatus for mass or heat transfer
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/30Details relating to random packing elements
    • B01J2219/319Mathematical modelling
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/33Details relating to the packing elements in general
    • B01J2219/3306Dimensions or size aspects

Definitions

  • the object underlying the invention was therefore the fouling of mass transfer columns to reduce and thus the distances between the required cleaning to enlarge.
  • the contact angle on the three-phase contact line between solid, liquid and gas can be determined according to WO 00/39 049, such as with the contact angle measuring device G1 from Krüss. This is done on the surface of the packing or the packing a drop of distilled water (approx. 20 ⁇ l) is added and the contact angle is read off measured on the goniometer scale. You wait from the application of the drop to the measurement three minutes to allow the system to equilibrate.
  • the static contact angle can be set with the aid of hydrophobizing substances.
  • the filling or packing body used according to the invention preferably has a surface structure particles attached to the surface with an at least bimodal particle size distribution, where a particle size range (A) is an average particle diameter of at least 5 ⁇ m and the other particle size range (B) is medium Has particle size diameter of at most 3 microns.
  • the weight ratio of the particles of the former particle size range (A) to the particles of the latter particle size range (B) assuming that these particles are each detached from the molded body Appropriately in the range from 0.01: 1 to 12: 1.
  • the particles are at least bimodal Particle size distribution from one piece with the molded body itself.
  • said particles in the particle size ranges (A) and (B) using a coating material to apply to the molded body.
  • Such coating materials that are suitable for fixing said particles on the surface of the shaped body, are in the WO 00/39 049.
  • WO 00/39 049 also describes molding compositions which have a pasty or pasty consistency can have and by known molding processes, such as by extrusion from a molded mouthpiece, by injection molding or the like, processed into moldings, which then Form molded body according to the invention.
  • This coating agent is usually a dispersion of binder, filler and optionally usual additives, preferably in aqueous dispersion.
  • the dispersion can also contain organic solvents, such as aliphatic or aromatic hydrocarbons, for example Toluene, esters or ketones, known as solvents for binders and paints are.
  • the binder contained expediently comprises, in each case based on the total weight of the Solids content of the molding or coating material, 0.2 to 20 wt.% At least one hydrophobic resin, resin precursor and / or wax and at least 0.5 to 40% by weight an additional hardening binder.
  • the hydrophobic resins or waxes used are preferably also oleophobic.
  • the Hydrophobic resins or waxes, preferably resins are expediently silicone resins which are used in In the case of aqueous dispersion must be emulsifiable or emulsified in water. Instead of silicone resins however, other resins, such as fluoropolymers, may also be used.
  • the resin intermediates can be, for example, silanes that polymerize to silicone resins. It is essential that these resins are hydrophobic. Waxes are inherently hydrophobic and can therefore, as a rule be used as a proportion of the hydrophobic binder.
  • the additional curing binders can be organic or inorganic in nature.
  • organic curing binders are alkyd resins, polyvinyl chloride, chlorinated rubber, Polyurethanes and epoxy resins.
  • inorganic curing binders are hydraulic binders such as cement or lime.
  • Organic polymers are preferably used as additional hardening binders.
  • the inorganic or organic fillers with at least bimodal particle size distribution are appropriately selected so that the particles of the former particle size range (A) have an average particle diameter in Range of 5 to 100 microns, preferably in the range of 8 to 40 microns, especially in the range from 10 to 40 ⁇ m, especially from 10 to 20 ⁇ m.
  • the particles of the latter particle size range (B) preferably have an average particle diameter of at most 0.1 ⁇ m, preferably in the range of 0.1 to 0.8 ⁇ m.
  • the coating materials can also still contain fillers of other particle size ranges and thus more than bimodal, i.e. H. have a multimodal particle size distribution. Especially in the case of cleaning additional portions of coarse grits may be present.
  • the average particle diameter is calculated from the sum of the largest particle diameters, divided by the number of the particles.
  • the weight ratio of the particles of the first particle size range (A) to the particles the last particle size range (B) is preferably in the range from 0.3: 1 to 10: 1, especially in the range from 1.0: 1 to 2.5: 1.
  • the fillers with at least bimodal particle size distribution can be a uniform filler of different particle sizes or filler mixtures be, in particular those in which the particle size range (A) of one Filler and the particle size range (B) is formed by another filler.
  • the particle size ranges (A) and (B) can each be of several different types of fillers are formed.
  • the fillers can be organic or inorganic Be natural, preferably inorganic.
  • the filler with the particle size range (A) can be, for example, silicon dioxide, calcium carbonate or Teflon.
  • the filler with the particle size range (B) can also silicon dioxide or for example Be titanium oxide. It is useful for the particle size range (A) and cristobalite Particle size range (B) titanium oxide, a colored pigment or a filler. It However, several fillers can also be used. Cristobalite is appropriately used as quartz flour used.
  • the binder suitably contains, based in each case on the solids content of the Coating material, preferably 1.5 to 30, particularly 2 to 15 wt.%, Very particularly to 6% by weight of additional hardening binder and 1 to 15, in particular 1.5 to 4% by weight hydrophobic resin, resin precursor or wax, especially silicone resin, silanes, siloxanes or Polysiloxanes.
  • binders that are as low as possible Contain water-soluble and / or hydrophilic substances such as emulsifiers and stabilizers.
  • Hardening binders which are expediently used are copolymers of acrylic and Methacrylic acid esters with styrene or ethylene vinyl laurate vinyl chloride.
  • Other useful curing agents Binders are pure acrylates, styrene acrylates and other preferably saponification-resistant Polymers or copolymers.
  • the silicone resins that can be used are for example those with alkyl or alkoxy groups, where they are preferably emulsifiable in water or are emulsified.
  • the customary additives which may have been added can optionally be hydrophobicized and are, for example, thickeners, such as polyurethane thickeners, wetting agents and / or defoamers, each conveniently in small amounts, especially in amounts below 2% by weight of the solids content of the coating composition are added.
  • thickeners such as polyurethane thickeners, wetting agents and / or defoamers

Landscapes

  • Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Paints Or Removers (AREA)
  • Prevention Of Fouling (AREA)
EP20030002949 2002-02-28 2003-02-11 Utilisation de corps moulés Expired - Lifetime EP1340536B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE10208930 2002-02-28
DE2002108930 DE10208930A1 (de) 2002-02-28 2002-02-28 Verwendung von Formkörpern

Publications (3)

Publication Number Publication Date
EP1340536A2 true EP1340536A2 (fr) 2003-09-03
EP1340536A3 EP1340536A3 (fr) 2004-06-16
EP1340536B1 EP1340536B1 (fr) 2009-04-15

Family

ID=27675144

Family Applications (1)

Application Number Title Priority Date Filing Date
EP20030002949 Expired - Lifetime EP1340536B1 (fr) 2002-02-28 2003-02-11 Utilisation de corps moulés

Country Status (2)

Country Link
EP (1) EP1340536B1 (fr)
DE (2) DE10208930A1 (fr)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2016133647A1 (fr) * 2015-02-17 2016-08-25 Exxonmobil Upstream Research Company Éléments de surface intérieure pour contacteurs à co-courant
US10130897B2 (en) 2013-01-25 2018-11-20 Exxonmobil Upstream Research Company Contacting a gas stream with a liquid stream
US10155193B2 (en) 2013-05-09 2018-12-18 Exxonmobil Upstream Research Company Separating impurities from a gas stream using a vertically oriented co-current contacting system
US10300429B2 (en) 2015-01-09 2019-05-28 Exxonmobil Upstream Research Company Separating impurities from a fluid stream using multiple co-current contactors
US10343107B2 (en) 2013-05-09 2019-07-09 Exxonmobil Upstream Research Company Separating carbon dioxide and hydrogen sulfide from a natural gas stream using co-current contacting systems
US10391442B2 (en) 2015-03-13 2019-08-27 Exxonmobil Upstream Research Company Coalescer for co-current contractors
US10876052B2 (en) 2017-06-20 2020-12-29 Exxonmobil Upstream Research Company Compact contacting systems and methods for scavenging sulfur-containing compounds
US11000797B2 (en) 2017-08-21 2021-05-11 Exxonmobil Upstream Research Company Integration of cold solvent and acid gas removal
US11000795B2 (en) 2017-06-15 2021-05-11 Exxonmobil Upstream Research Company Fractionation system using compact co-current contacting systems
US11260342B2 (en) 2017-06-15 2022-03-01 Exxonmobil Upstream Research Company Fractionation system using bundled compact co-current contacting systems

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CH268258A (fr) * 1946-07-30 1950-08-16 Rhone Poulenc Chemicals Revêtement hydrofuge.
DE19803787A1 (de) * 1998-01-30 1999-08-05 Creavis Tech & Innovation Gmbh Strukturierte Oberflächen mit hydrophoben Eigenschaften
DE29923250U1 (de) * 1998-12-24 2000-08-31 ispo GmbH, 65830 Kriftel Form- oder Beschichtungsmaterial
DE10162457A1 (de) * 2001-12-19 2003-07-03 Degussa Oberflächenstrukturierte Einbauten für Mehrphasentrennapparate

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10130897B2 (en) 2013-01-25 2018-11-20 Exxonmobil Upstream Research Company Contacting a gas stream with a liquid stream
US10155193B2 (en) 2013-05-09 2018-12-18 Exxonmobil Upstream Research Company Separating impurities from a gas stream using a vertically oriented co-current contacting system
US10343107B2 (en) 2013-05-09 2019-07-09 Exxonmobil Upstream Research Company Separating carbon dioxide and hydrogen sulfide from a natural gas stream using co-current contacting systems
US10300429B2 (en) 2015-01-09 2019-05-28 Exxonmobil Upstream Research Company Separating impurities from a fluid stream using multiple co-current contactors
WO2016133647A1 (fr) * 2015-02-17 2016-08-25 Exxonmobil Upstream Research Company Éléments de surface intérieure pour contacteurs à co-courant
US10391442B2 (en) 2015-03-13 2019-08-27 Exxonmobil Upstream Research Company Coalescer for co-current contractors
US10486100B1 (en) 2015-03-13 2019-11-26 Exxonmobil Upstream Research Company Coalescer for co-current contactors
US11000795B2 (en) 2017-06-15 2021-05-11 Exxonmobil Upstream Research Company Fractionation system using compact co-current contacting systems
US11260342B2 (en) 2017-06-15 2022-03-01 Exxonmobil Upstream Research Company Fractionation system using bundled compact co-current contacting systems
US10876052B2 (en) 2017-06-20 2020-12-29 Exxonmobil Upstream Research Company Compact contacting systems and methods for scavenging sulfur-containing compounds
US11000797B2 (en) 2017-08-21 2021-05-11 Exxonmobil Upstream Research Company Integration of cold solvent and acid gas removal

Also Published As

Publication number Publication date
DE10208930A1 (de) 2003-09-11
EP1340536A3 (fr) 2004-06-16
DE50311406D1 (de) 2009-05-28
EP1340536B1 (fr) 2009-04-15

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